AU2021276502A1

AU2021276502A1 - Ketone functionalized polymers, methods of making ketone functionalized polymers, and compositions including the same

Info

Publication number: AU2021276502A1
Application number: AU2021276502A
Authority: AU
Inventors: Haibo Li; Matthew Swenson
Original assignee: Ennis Flint Inc
Current assignee: Ennis Flint Inc
Priority date: 2020-05-20
Filing date: 2021-05-20
Publication date: 2023-01-19
Anticipated expiration: 2041-05-20
Also published as: US20230227687A1; AU2021276502B2; MX2022014428A; EP4153644A2; CA3177555A1; WO2021236883A3; WO2021236883A2

Abstract

A ketone-containing polymer can provide for a paint having increased scrub resistance and decreased changes in viscosity, while maintaining quick dry times. In particular, the polymers may be used in compositions for traffic markings and industrial coatings.

Description

KETONE FUNCTIONALIZED POLYMERS, METHODS OF MAKING KETONE FUNCTIONALIZED POLYMERS, AND COMPOSITIONS INCLUDING THE SAME

CROSS-REFERENCE TO RELATED APPLICATIONS [0001] This application claims priority to U.S. Provisional Application No. 63/027,568, filed May 20, 2020, which is incorporated herein by reference in its entirety for all purposes.

FIELD

[0002] Described herein are polymers, and polymers used in paint or coating compositions. In some aspects the compositions described herein can be usefttl for roadway markings.

BACKGROUND

[0003] Paint or coating compositions can have a wide range of applications. In applications such as traffic markings and industrial coatings, durability and drying time may be considerations when selecting a paint or coating composition.

[0004] Polyfunctional amine (PFA) in paint or coating compositions, such as waterborne paints, have been used to impart better dry time and/or better water resistance. However, these paint or coating compositions can exhibit limited paint stability and low scrub resistance. Furthermore, known paint or coating compositions with suitable stability and/or scrub resistance may exhibit undesirably high dry times. The combination of stability, scrub resistance, and suitable dry time is particularly useful in certain applications, such as in fast dry waterborne coating, waterborne adhesives and sealants.

SUMMARY

[0005] The present disclosure provides a polymer according to Formula 1 :

Formula 1 wherein each of m, n, and p is independently a number from 0.5 to 500; each of R₁, R₂. and R₃ is independently -H or C₁-C₄ alkyl; R₄ is an amine-substituted C₁-C₆ alkyl; R₅ is -H or C·- C₆ alkyl; R_<, is substituted or unsubstituted C₁-C₆ alkyl; each of X₁ X₃, X₅, and X₆ is independently S, O, or N; each of X2, X4, X7, and Xs is independently S or O; Y is CH₂, CS, or CO; and each of L₁ and L₂ is independently substituted or unsubstituted C₁-C₆ alkyl.

[0006] The present disclosure also provides a polymer formed from the formed by- reacting a mixture comprising the following monomers:

[0007] The present disclosure also provides a polymer according to Formula 2: wherein each of m, n, and p is independently a number from 0.5 to 500; each of R₁, R₂, and R₃ is independently -H or C₁-C₄ alkyl; R4 is an amine-substituted C₁-C₆ alkyl; R5 is -H or C1 C 6alkyl; each of X₁ and X3 is independently S, O, or N; each of X2, X4, and X₆, is independently S or O; each of a and b is independently a number from 0 to 4; and L₁ is -H or substituted or unsubstituted C₁-C₆ alkyl. DETAILED DESCRIPTION

[0008] Paints and coating compositions with high stability and good scrub resistance without the loss of advantages dry time may be achieved with the polymers described herein. Polymers having a structure according to Formula 1 are disclosed herein:

Formula 1 wherein each of m, n, and p is independently a number from 0.5 to 500; each of R₁, R2, and R₃ is independently H or C₁-C₄ alkyl; R₄ is an amine-substituted C₁-C₆ alkyl; R₅ is H or C₁-C₆, alkyl; Rg is substituted or unsubstituted C₁-C₆ alkyl; each of X₁, X₃, X_.5 and X₆ is independently S, O, or N; each of X2, X4, X₇, and X8 is independently S or O; Y is CH₂, CO, or CS; and each of L₁ and L₂ is independently substituted or unsubstituted C₁-C₆ alkyl.

[0009] Polymers may be formed from the reaction mixture comprising the following monomers: [0010] Polymers may have a structure according to Formuia I :

Formula 1 where each of m, n, and p is independently a number from 0.5 to 500; each of R₁, R₂, and R:, is independently -H or C₁-C4 alkyl; R4 is an amine-substituted C₁-C₆ alkyl; R; is -H or C₁-C₆, alkyl; Re is substituted or unsubstituted C₁-C₆ alkyl; each of X₁, X3, X₅, and X₆ is independently S, O, or N; each of X2, X4. X7, and Xg is independently S or O; Y is CH₂, CO, or CS; and each of L₁ and L₂ is independently substituted or unsubstituted C₁-C₆ alkyl.

[0011] The polymers can be referred to as Ketone-Polyfunctional Amine (“Ketone-PFA”) polymers.

[0012] R4 may be selected from the group consisting of-CH₂CH₂NH₂, - CH₂CH₂N(CH3)2 , and -CH₂CH₂N(CH₂CH3)₂.

[0013] L₁ and L₂ may be independently selected from the group consisting of -CH₂-; - CH₂CH₂-; and -CH₂CH₂CH₂-. Optionally, L₁ may be -CH₂CH₂-.

[0014] R6 may be -CH₃. Each of X₁ to X8 may be O, and Y may be CO. Each of R₁-R₃ may be -CH3.

[0015] The polymer may have a structure according to Formula lx: Formula lx wherein each of R₁, R₂, and R₃ is independently H, CH3, or CH₂CH₃. In the polymer, m may be from 80 to 200, n may be 10 to 20, and p may be 0.5 to 4.

[0016] The polymer may have a structure according to Formula 2: where each of m, n, and p is independently a number from 0.5 to 500; each of R₁, R₂, and R3 is independently -H or C₁-C₄ alkyl; R4 is an amine-substituted C₁-C₆ alkyl; R5 is -H or C₁-C₆ alkyl; each of X₁ and X3 is independently S, O, or N; each of X2 X₄, and X6_, is independently S or O; each of a and b is independently a number from 0 to 4; and L₁ is -H or substituted or unsubstituted C₁-C₆ alkyl.

[0017] The polymers can be derived from acrylate, methacrylate, or ethacrylate monomers, or a mixture thereof.

[0018] The polymers can be random copolymers. The subscripts m, n, and p represent the average number of specific types of monomer units incorporated in the copolymer as repeat units.

[0019] Numbers m, n, and p represent the average number of the designated repeat units in the polymer chain. In cases where m, n, or p has a value of less than one, then a fraction of the polymer chains contain the designated repeat unit. The value of m can be from 50 to 500, from 60 to 400, from 80 to 200, from 90 to 180, or from 100 to 150. The value of n can be from 5 to 50, from 6 to 45, from 7 to 40, from 8 to 30, from 8 to 20, or from 10 to 15. The value of p can be from 0.5 to 4, from 0.6 to 3.5, from 0.7 to 3, from 0.8 to 2.5, or from 1 to 2. The ratio of m:p can be any number between 20 and 400. The ratio of n:p can be any number between 2 and 40. The ratio of m:n:p can be about 50:5:1 or about 150:20:1.

[0020] The polymers can be formed from a reaction mixture comprising certain monomers. In cases where a ketone-containing monomer is used, the resulting polymer is called a Ketone-containing polymer. If an amine-containing monomer is used in addition to the ketone-containing monomer, the resulting polymer is called a Ketone- Amine polymer. More specifically, if polyfimctional amine-containing monomer is used in addition to the ketone-containing monomer, the resulting polymer is called a Ketone-PFA polymer.

[0021] The reaction mixture may comprise a ketone-containing monomer and an amino- containing monomer. The ketone-containing monomer may comprise more than one ketone moiety per monomer. The ketone-containing monomer can comprise 2, 3, 4, 5 or 6 ketone moieties per monomer.

[0022] The presence of the amino-containing monomer may improve the performance characteristics of the PFA as well as the compositions formed therefrom. In certain environments (e.g., at appropriate pH, as described below), the amino groups along the PFA may be positively charged. The positively charged amino groups may attract other components of the compositions (e.g., latex particles), facilitating film formation.

[0023] Any ketone-containing monomer can be used for the polymer. A ketone- containing monomer such as 2-(Methacryioyloxy)ethyl acetoacetate (AAEM), Diacetone acrylamide (DAAM), allyl acetoacetate (AAA), 2-(Acryloyloxy)ethyl acetoacetate (AAEA), methyl vinyl ketone (MVK), ethyl vinyl ketone (EVK), allyl acetone, acrolein, and/or methacrolein, may be used. Ketone-containing monomers based on acrylic acid, methyl acrylate, ethyl acrylate, propyl acrylate, and butyl acrylate monomers may be used.

[0024] The amine-containing monomer may comprise one or more amino moieties per monomer. The amino moieties can be primary amine groups, secondary amine groups, or tertiary amine groups. In some examples, the amine-containing monomer may comprise more than one amino moiety per monomer. The amine-containing monomer may comprise 2, 3, 4,

5 or 6 amino moieties per monomer. In this case, each amino moiety of the amine-containing monomer may independently be a primary amine group, a secondary amine group, or a tertiary amine group.

[0025] Any amine-containing monomer can be used. Amine-containing monomers such as 2-(Dimethylamino)ethyl methacrylate (DMAEMA), 2-(Dimethylamino)ethyl acrylate (DMAEA), 3-(Dimethy!ammo)propy! acrylate (DMAPA), 2-(Diethylamino)ethyl acrylate (DEAEA), 2-(Diethylamino)ethyl methacrylate (DEAEMA), 2-(Diisopropylamino)ethyl methacrylate (DIAEMA), N-3-(Dimethyiamino)propyhnethacrylamide (N-DMAPMA), and 2-N-Morpholinoethyl methacrylate (MEMA) may be used.

[0026] Additional monomers may be included in the reaction mixture. Particular examples include maleic acid (MA), maleic anhydride (MAHD), iumaric acid (FA), and methacrylic acid (MAA). MAHD and/or FA may be substituted for MA, and the reaction mixture may be essentially free of MA. [0027] The polymers may be formed from a reaction mixture comprising the following monomers:

The polymers may be formed from a reaction mixture comprising the following monomers:

The reaction mixture may further comprise one or more of the following monomers: or combinations thereof.

[0028] Disclosed herein are methods of making ketone functionalized polymers. A polymerization reaction mixture may further comprise one or both of the following monomers:

[0029] A solution comprising water and maleic anhydride can be prepared in a vessel. Fumaric acid and/or maleic acid may be substituted for some or all of the maleic anhydride. The prepared solution may comprise an aqueous solution of maleic anhydride, fumaric acid and/or maleic acid in an amount of from 0.1 wt. % to 10 wt. % based on the total weight of the prepared solution. The prepared solution may comprise an aqueous solution of maleic anhydride, fumaric acid and/or maleic acid in an amount of from 0.1 wt. % to 8 wt. %, from 0.1 wt. % to 5 wt. %, from 0.1 wt. % to 3 wt. %, from 0.5 wt. % to 8 wt. %, from 0.5 wt. % to 5 wt. %, from 0.5 wt. % to 3 wt. %, from 1 wt. % to 8 wt. %, from 1 wt. % to 5 wt. %, or from 1 wt. % to 3 wt. %.

[0030] A monomer suspension can formed by placing a ketone-containing monomer and an amine-containing monomer in water. The monomer suspension may comprise additional monomers, such as MMA. The monomer solution may be added to the prepared solution. [0031] The monomer solution may comprise a monomer suspension of DMAEMA, AAEM, and/or MAA. DMAEMA may be present from 60 wt. % to 98 wt. % in the monomer suspension. DMAEMA may be present in the monomer suspension in an amount from 70 wt. % to 95 wt. % of the monomer suspension, e.g., from 75 wt. % to 90 wt. %. AAEM may be present from 0.2 wt. % to 5 wt. % in the monomer solution. AAEM may be present in the monomer suspension in an amount of from 0.5 wt. % to 4 wt. % of the monomer solution, e.g., from 0.75 wt. % to 3 wt. % or from 1 wt. % to 3 wt. % of the monomer solution. In cases where MAA is present, it may be present in the monomer solution in an amount of up to 5 wt. % of the monomer solution , e.g., up to 10 wt. % or up to 15 wt. %. Maleic acid, which may be charged to reactor, may be mixed in the monomer solution as well.

[0032] An initiator solution (e.g., a redox initiator) may be added to the vessel. Multiple redox initiator solutions may be added to the vessel. The initiator solution and the redox initiator may be added to the vessel at the same period of time, or at a different period of time. The reaction mixture may comprise less than 20 vol. % of the initiator solution. [0033] The reaction can be conducted at a temperature of from 1 °C to 90 °C. The reaction may begin at ambient conditions. As used herein, “ambient conditions” refers to room temperature, e.g., from 20 °C to 30 °C. The reaction maybe exothermic in nature.

[0034] The reaction can be initiated by a thermal free radical initiator. Any known free radical initiator may be used. The free radical initiator may be selected from the group consisting of ammonium persulfate (APS), azobisisobutyronitrile (AIBN), benzoyl peroxide, acetyl peroxide, and t-butyl peracetate. The free radical initiator may be ammonium persulfate. The free radical initiator may be azobisisobutyronitrile.

[0035] The reaction can be initiated by a free radical initiator created reducing-oxidizing (red-ox) initiation. The reaction can be initiated by a reducing-oxidizing pair of initiators comprising an oxidizing agent and a reducing agent. Any known reducing-oxidizing pair of initiators may be used. Non-limiting examples of the oxidizing agent may include hydrogen peroxide, tert- butyl hydroperoxide (tBHP), ammonium persulfate (APS), sodium persulfate (SPS) and potassium persulfate (PPS). Non-limiting examples of the reducing agent may include a sulfuric acid derivative formaldehyde free reducing agent such as Bruggolite FF6M (available from Briiggemann), disodium hydroxysulfmoacetate (Bruggolite FF7), sodium salt of an organic sulfinic acid derivative such as Bruggolite E28 (available from Briiggemann), sodium formaldehyde sulfoxylate (Bruggolite E01), a stabilized solution of sodium formaldehyde sulfoxylate (Bruggolite L40), Bruggolite TP 1651 (available from Briigge- mann), ascorbic acid, sodium formaldehyde sulfoxylate (SFS), sodium bisulfite, and sodium metabisulfite (SMBS).

[0036] The oxidizing agent may be present in an aqueous oxidizing solution in an amount of from 0.2 to 5 wt. %, based on total monomer weight. The reducing agent may be present in an aqueous reducing solution in an amount of from 0.2 to 5 wt. %, based on total monomer weight. The weight ratio of the oxidizing agent to the reducing agent may be from 0.5:1 to 2: 1.

[0037] In another aspect, the polymers disclosed herein may be used as additives in coatings, for example, paint.

[0038] It will be recognized by one of ordinary skill in the art that the latex formulations described herein may be used as water-borne paints, or that the latex particles might be dried or otherwise purified and used in low- or non-aqueous coating applications. The coating compositions can comprise the polymers disclosed herein and an amine-containing compound. The amine-containing compound may comprise an amine-containing polymer. The amine-containing compound may comprise a silyl amine. [0039] The polymers described herein may be used as performance-enhancing additives in coating compositions, including water-borne paints for traffic marking. Ketone-PFA polymers can be used as additives in an amount of less than 2 wt. %, less than 1.5 wt. %, less than 1 wt. %, less than 0.9 wt. %, or less than 0.5 wt. %, based on the total weight of the water-borne paints. Ketone-PFA polymers can be used as additives in an amount of from 0.1 to 2 wt. %, from 0.25 to 1.5 wt. %, from 0.5 to 1.5 wt. %, or from 0.5 to 1 wt. %, based on the total weight of the 'water-borne paints.

[0040] The polymers described herein may be used as performance-enhancing additives in high-build coating compositions. High-build coating compositions comprising Ketone- PFA polymers can be applied at a thickness of at least 5 mils, e.g., at least 10 mils, at least 15 mils, at least 20 mils, at least 25 mils, at least 30 wet mils, at least 40 mils, or at least 50 mils. [0041] The coating compositions comprising Ketone-PFA polymers may further comprise an amine-containing compound. The amine-containing compound may comprises an amine-containing polymer. The amine-containing compound may comprise a siiyl amine. The amine functionality of a siiyl amine additive can react with the ketone functionality in the Ketone-PFA polymer additive to cross-link and strengthen the paint formulation.

[0042] Organic compounds carrying a primary or secondary amino group and siiyl group that is categorized as a “siiyl amine” can be used with the compositions provided herein. Optionally, the silyl amines can be selected from the group consisting of N-[3- (Trimethoxysilyl)propyl]ethylenediamine, N1 -(3-Trimethoxysilylpropyl)diethylenetriamine, G-A minopropyljtrimethoxysilane, (3-Aminopropyl)triethoxysiiane, 3- (Ethoxydimethylsilyl)propylamine, andN-[3-(Trimethoxysilyl)propyl]ethylenediamine. The siiyl amine may be aminoethylaminopropyl trimethoxysilane.

[0043] Polymeric or oligomeric ethylene imines serving as siiyl amine alternatives may be used instead of, or in addition to, the siiyl amines listed above. A list of suitable polymeric and oligomeric ethylene imines include, but are not limited to, linear polyethylene imine) (PEI), dendritic or branched poly(ethylene imine) (PEI), low molecular weight ethylene diamine (EDA), diethylene triamine (DETA), triethylene tetraamine (TETA), tetraethylene pentamine (TEPA), and pentaethylene hexamine (PEHA).

[0044] The siiyl amines may be used as additives in an amount of less than 1 wt. %, less than 0.5 wt. %, less than 0.4 wt. %, less than 0.3 wt. %, less than 0.2 wt. %, or less than 0.1 wt. %, based on the total dry weight of the water-borne paints. Dry weight refers to the weight of the solid components in the water-borne paint. The siiyl amines may be used as additives in an amount of from 0.01 to 0.5 wt. %, from 0.005 to 0.5 wt. %, from 0.05 to 0.5 wt. %, or from 0.000001 to 0.5 wt. %, based on the total weight of the water-borne paints. Optionally, no silyl amine additive may be present,

[0045] Known latex additives may be present in some coating compositions. Examples may include, but are not limited to dispersants, nonionic surfactants, defoamers, viscosity modifiers, water, titanium dioxide (TiO₂), calcium carbonate (CaCO3), methanol (MeOH), coalescing solvents, and float solvents.

[0046] Ketone-PFA polymers can be used in a coating composition comprising a latex paint that is amonically stabilized, such as the latex described in Example 3, below.

[0047] The consistency of paints and coatings may be measured using a Stormer-type viscometer to determine Krebs Unit (KU) viscosity according to ASTM D562-10 (2018), “Standard Test Method for Consistency of Paints Measuring Krebs Unit (KU) Afiseosity Using a Stormer-Type Afiscometer.” Using ASTM D562-10, the initial KU and delta KU can be measured. Initial KU refers to viscosity of fresh made paints, and delta KU refers to viscosity" of paints being set at 63 °C for one week The coating composition may have a delta KU (Krebs Unit) value of less than 15 KU, less than 14 KU, less than 13 KU, less than 12 KU, less than 11 KU, less than 10 KU, less than 9 KU, less than 8 KU, less than 7 KU, or less than 6 KU.

[0048] Dry time of the paints and coatings may be determined according to ASTM D711- 20 (2015), “Standard Test Method for No-Pick-Up Time of Traffic Paint.” The coating compositions may" have a dry" time of less than 10 minutes, less than 9 minutes, less than 8 minutes, less than 7 minutes, less than 6 minutes, less than 5 minutes, or less than 4 minutes. [0049] Scrub Resistance of the paints and coatings may be determined according to ASTM D2486-00 (2000), “Standard Test Methods for Scrub Resistance of Wall Paints.” The coating compositions may have a scrub resistance of greater than or equal to 100% relative to a control sample of a conventional paint. The coating composition may have a scrub resistance of greater than or equal to 105%, greater than or equal to 110%, greater than or equal to 115%, greater than or equal to 120%, greater than or equal to 125%, greater than or equal to 130%, greater than or equal to 135%, or greater than or equal to 140% relative to the control.

[0050] As used herein, the terms alkyl, alkenyl, and alkynyi include straight- and branched-chain monovalent substituents. Examples include methyl, ethyl, isobutyl, 3- butynyl, and the like. [0051] The term alkoxy as used herein is an aikyl group bound through a single, terminal ether linkage. The term aryloxy as used herein is an aryl group bound through a single, terminal ether linkage. Likewise, the terms a!kenyloxy, alkynyloxy, heteroalkyloxy, heteroalkenyloxy, heteroalkynyloxy, heteroaryloxy, cycloalkyloxy, and heterocycloalkyloxy as used herein are an alkenyloxy, alkynyloxy, heteroalkyloxy, heteroalkenyloxy, heteroalkynyloxy, heteroaryloxy, cycloalkyloxy, and heterocycloalkyloxy group, respectively, bound through a single, terminal ether linkage.

[0052] The term hydroxy as used herein is represented by the formula — OH.

[0053] The terms amine or amino as used herein are represented by_^ the formula — NZ‘Z², where Z¹ and Z can each be substitution group as described herein, such as hydrogen, an alkyl, halogenated alkyl, alkenyl, aikynyl, aryl, heteroaryl, cycloalkyl, cycloalkenyl, heterocycloalkyl, or heterocycloalkenyl group described above.

[0054] The alkoxy, aryloxy. amino, alkyl, alkenyl, aikynyl, aryl, heteroa!kyl, heteroalkenyl, heteroalkynyl, heteroaryl, cycloalkyl, or heterocycloalkyl molecules used herein can be substituted or unsubstituted. As used herein, the term substituted includes the addition of an alkoxy, aryloxy , amino, alkyl, alkenyl, aikynyl, aryl, heteroalkyl, heteroalkenyl, heteroalkynyl, heteroaryl, cycloalkyl, or heterocycloalkyl group to a position attached to the main chain of the alkoxy, aryloxy, amino, alkyl, alkenyl, aikynyl, aryl, heteroalkyl, heteroalkenyl, heteroalkynyl, heteroaryl, cycloalkyl, or heterocycloalkyl, e.g., the replacement of a hydrogen by one of these molecules. Examples of substitution groups include, but are not limited to, hydroxy, halogen (e.g., F, Br, Cl, or I), and carboxyl groups. Conversely, as used herein, the term unsubstituted indicates the alkoxy, aryloxy, amino, alkyl, alkenyl, aikynyl, aryl , heteroalkyl, heteroalkenyl, heteroalkynyl, heteroaryl, cycloalkyl, or heterocycloalkyl has a full complement of hydrogens, i.e., commensurate with its saturation level, with no substitutions, e.g., linear decane (-(Cf-hy-CH i).

[0055] As used herein, unless otherwise expressly specified, all numbers such as those expressing values, ranges, amounts or percentages may be read as if prefaced by the word "about", even if the term does not expressly appear. Any numerical range recited herein is intended to include all subranges subsumed therein. Plural encompasses singular and vice versa. For example, while the invention has been described in terms of "a” polymer according to Formula 1, a mixture of such polymers can be used. Also, as used herein, the term "polymer" is meant to refer to prepolymers, oligomers and both homopolymers and copolymers; the prefix "poly" refers to two or more. When ranges are given, any endpoints of those ranges and/or numbers within those ranges can be combined within the scope of the present invention. Including and like terms means “including but not limited to”.

[0056] The word “comprising” and forms of the word “comprising” as used in this description and in the claims does not limit the invention claimed to exclude any variants or additions.

[0057] Although the invention has been described in terms of “comprising”, “consisting essentially of’ or “consisting of’ are also within the scope of the present invention. For example while the invention has been described in terms of a coating composition comprising a polymer (or polymers) described herein and an amine-containing compound, a coating composition consisting essentially of and/or consisting of the polymer (or polymers) and the amine-containing compound is also within the present scope. In this context, “consisting essentially of” means that any additional coating components will not materially affect the viscosity, dry time, and or scrub resistance of the coating.

EXAMPLES

[0058] Notwithstanding that the numerical ranges and parameters setting forth the broad scope of the invention are approximations, numerical values set forth in the specific examples are reported as precisely as possible. Any numerical value, however, inherently contains certain errors necessarily resulting from the standard variation found in their respective testing measurements.

Example 1: Preparation of Ketone-PFA Polymer

[0059] An exemplary Ketone-PFA polymer was prepared according to the following method. Table 1 provides the amounts of each component used to form an exemplary Ketone-PFA polymer.

Table 1: Reagents for Preparation of Ketone-PFA Polymer [0060] Bmggolite FF6 is commercially available from Bruggemann (Heil-bronn, Germany).

[0061] Preparation steps:

[0062] Maleic acid and water were charged to a vessel.

[0063] In a monomer vessel, 2-(Dimethylamino)ethyI methacrylate (DMAEMA), 2- (Methacryloyloxy)ethyl acetoacetate (AAEM), and (Meth)acry!ic acid (MAA) were combined. The oxidizer solution and reducer solution were prepared in separate vessels. The reducer solution was agitated as needed to dissolve the Bmggolite FF6.

[0064] The vessel temperature was maintained at 25 °C, while a simultaneous co-feed of monomer, oxidizer and reducer solutions was provided to the vessel. The monomer solution was added over a 120 minute period. The monomer vessel was rinsed with water, and the rinse water was added into the vessel. The oxidizer and the reducer solutions were added over a 240 minute period.

[0065] The temperature of the reaction mixture increased due to the exothermic nature of the reaction. No extra measures were taken to control temperature of the reactions.

[0066] The above procedure produced a product of ketone functional polyfunctionai amine (Ketone-PFA) of 30 wt. % in water, as determined by a Sartorius Mark 3 moisture analyzer.

Example 2: Preparation of Comparative PFA Polymer Without Ketone Functionality [0067] A comparative PFA polymer without ketone functionality was prepared according to the following method. Table 2 provides the amounts of each component used to form an comparative PFA polymer.

Table 2: Reagents for Preparation of Comparative PFA Polymer

[0068] Preparation steps:

[0069] Water was charged to a 3 liter jacketed glass reactor. A Julabo circulator was used to circulate w'ater through the jacket and heat the reactor to 55 °C. [0070] The monomer solution, oxidizer solution, and reducer solution were prepared in separate vessels.

[0071] The reactor was heated to a temperature of 55 °C. During the heat-up, the monomer solution, the oxidizer solution, and the reducer solution were simultaneously co-fed to the reactor. The monomer solution was added over a 120 minute period. Once the monomer charge was complete, the monomer vessel was rinsed with water and the rinse water added to the reactor. The oxidizer solution and the reducer solution were added over a 240 minute period.

[0072] The above procedure produced a comparable polyfunctional amine (PFA) product of 24-27 wt. % in water, as determined by a Sartorius Mark 3 moisture analyzer.

[0073] In-situ hydrolysis of the DMAEMA gave rise to a MAA repeating unit in the polymer that resulted in a poly(DMAEMA-MAA) copolymer. This product was used as the control in the comparative coating formulation described in Example 4.

Example 3: Preparation of a Latex Resin as a Base Formulation for Water-Borne Paints [0074] A latex resin to use a base formulation for water borne paints was prepared according to the following method. Table 3 provides the amounts of each component in preparation of the latex resin.

Table 3; Reagents for Preparation of a typical Latex Resin base formulation

[0075] Materials:

[0076] The seed latex solution was prepared as described below.

[0077] Proxel GXL biocide is commercially available from Lonza (Basel, Switzerland).

[0078] The seed latex solution was previously prepared, in a 3 liter reactor. The reactor was charged with 210.9 g of a sodium dodecyl sulfate (SDS) solution (14% of the total solution), 4.6 g of Sodium bicarbonate (NaHCO₃), 503.3 g of water, 158.0 g of BA, 189.5 g of MMA, 6.8 g of MAA and 16.2 g of APS. The seed solution was heated to 65 °C while the solution was agitated. The exothermic radical polymerization was controlled using 353.2 g of water that was added gradually over a period of four minutes. The seed solution was allowed to react for another 130 minutes. The latex particle size obtained was 51 nm, as determined by transmission dynamic light scattering.

[0079] Preparation steps:

[0080] Ammonium carbonate and water were charged to a 3 liter jacketed glass reactor.

A Julabo circulator was used to circulate water through the jacket and heat the reactor to 83 °C.

[0081] While the reactor was heating, the reagents for the monomer emulsion were charged to a 2-liter glass vessel. The mixture was agitated to produce a stable homogeneous white emulsion.

[0082] The initiator solution was prepared by dissolving APS in a vessel containing water.

[0083] The reactor APS solution was prepared by dissolving APS in a vessel containing water.

[0084] When the ammonium carbonate solution in the reactor reached 80 °C, the seed latex solution and the reactor APS solution were charged to the reactor. The charge vessels were rinsed with water and the rinse water added to the reactor to avoid material loss during the additions.

[0085] The addition of the seed latex solution and the reactor APS solution resulted in a temperature drop of the reaction mixture. The reactor was reheated to 80 °C. Once the reactor was on temperature, the charge of monomer emulsion and initiator solution was started.

[0086] The monomer emulsion and initiator solution were added over a 195 minute period. Peristaltic pumps equipped with rubber tubes were used to feed monomer emulsion and initiator solutions to the reactor. The feed rate for monomer was maintained such that the feed rate (in grams/minute) of the first 30 minutes was half of the rate of the feed for the remaining 165 minutes to avoid an uncontrolled exotherm in early polymerization stage. The feed rate of the initiator solution was constant. During polymerization stage or monomer emulsion feed-in stage, the reaction temperature was maintained between 80-85 °C.

[0087] Upon completion of monomer emulsion feed, the chaser solution was prepared and fed into the reactor with peristaltic pump over a period of one hour.

[0088] The reaction was cooled to below 40 °C. A diluted solution of ammonium hydroxide in water was prepared and added slowly into the reactor over a period of 5 minutes. GXL biocide was added to the reactor to conclude the preparation of the latex resin. [0089] The resulting latex resin had a pH between 10.0- 10.5, average particle size of 220 urn, and solids content of 50.0%. Tg of the later polymer was in the range of 23-28 °C,

Example 4: Inventive and Comparative Paint Formulations [0090] Paint formulations w'ere made using the Ketone-PFA from Example 1 , the comparative PFA polymer of Example 2, and the latex resin of Example 3. The paint formulations were prepared according to the following method. Table 4 provides the amounts of each component used in preparation of the paint formulations. As shown in Table 4, the differences between the various paint formulations are the respective amounts of Ketone- PFA, silyl amine, or PFA polymer therein.

Table 4: Components of Inventive and Comparative Paint Formulations

[0091] Materials: The latex resin of Example 3 was used for Example Paints 1-5. The Ketone-PFA polymer of Example 1 was used in Example Paints 1-4. The PEA polymer without ketone functionality of Example 2 was used in Comparative Paint 5.

Paint formulation process for Example Paints 1-4:

[0092] The Ketone-PFA was added to a quart can containing 455.1 g of the latex resin. The latex mixture was stirred for 5 minutes using a high sheer mixing blade at moderate speed. The silyl amine was added to the latex mixture dropwise while the agitation was maintained. After 5 additional minutes, the dispersant, the nonionic surfactant, and the defoamer were added while the latex mixture was stirred with a high sheer mixing blade at a moderate speed for 5 minutes. A solution of the viscosity modifier in the water was added to the latex mixture and the latex mixture was stirred at high speed for 5 minutes. Additional ammonium hydroxide (30% by weight in water) was added as needed to ensure a minimum pFI of 10.0. TiOz and CaCO₃ were then added to the mixture while stirring at high speed for 15 minutes. After completion of the mixing and particle size of the solid materials reduced by grinding, MeOH was added slowly at a reduced stirring speed. The coalescing solvent was then added to the latex mixture with continuous stirring. Finally, the waterborne floating solution was added and stirred into the latex mixture and the latex mixture was stirred for another 5 minutes until the Example Paints were complete.

Paint formulation process for Comparative Paint 5:

[0093] The PFA without ketone functionality of Example 2 was added to a quart can containing 455.1 g of the latex resin . The latex mixture w^ras stirred for 5 minutes using a high sheer mixing blade at moderate speed. After 5 additional minutes, minutes, the dispersant, the nonionic surfactant, and the defoamer were added while the latex mixture was stirred with a high sheer mixing blade at a moderate speed for 5 minutes. A solution of the viscosity modifier in the water was added and the latex mixture was stirred at high speed for 5 minutes. Additional ammonium hydroxide (30% by weight in water) was added as needed to ensure a minimum pH of 10.0. TiO₂ and CaCO₃ were then added while stirring at high speed for 15 minutes. After completion of the mixing and particle size of the solid materials reduced by grinding, MeOH was added slowly at a reduced stirring speed. The coalescing solvent was then added to the latex mixture with continuous stirring. Finally, the water borne floating solution was added and stirred into the latex mixture and the latex mixture was stirred for another 5 minutes until the Comparative Paint was complete.

Paint formulation process for Comparative Paint 6:

[0094] A quart can containing 455.1 g of commercially available latex resin was stirred for 5 minutes using a high sheer mixing blade at moderate speed. After 5 additional minutes, the dispersant, the nonionic surfactant, and the defoamer were added while the latex was stirred with a high sheer mixing blade at a moderate speed for 5 minutes. Next, a solution of the viscosity modifier in the water was added and the latex was stirred at high speed for 5 minutes. Ammonium hydroxide (30% by weight in water) was added as needed to ensure a minimum pH of 10.0. TiO₂ and CaCO₃ were then added while stirring at high speed for 15 minutes. After completion of the mixing and particle size of the solid materials reduced, MeOH was added slowly at a reduced stirring speed. The coalescing solvent was then added to the mixture with continuous stirring. Finally, the water borne floating solution was added and stirred into the mixture and the mixture was stirred for another 5 minutes until Comparative Paint 6 was complete.

[0095] The amount of Ketone-PFA, PFA without ketone functionality, and Silyl Amine additi ves based on the total weight of the paint formulation, are listed in Table 5.

Table 5 Example 5: Testing of Example and Comparative Paint Formulations [0096] The scrub resistance of the paint formulations was tested according to ASTM D2486-00. Paint made from a commercially available latex (Comparative Paint 6) was used as the control. Higher scrub resistance performance reflects longer durability when paint films were scrubbed under mechanical force.

[0097] The viscosity of the paints was tested according to ASTM D562-10 (2018). Kreb unit number or KU was been used to record the viscosity of the paints. Initial KU refers to viscosity of fresh made paints, and delta KU refers to viscosity of paints being set at 63 °C for one week. Prior to measurement using a Kreb unit viscometer, the paints were equilibrated at a 25 °C w'ater bath for 30 minutes. Lower delta KU generally reflects better stability of paints with lower change in viscosity over the trial period.

[0098] For the scrub test, a sample of paint was drawn to 15 mil w^ret film thickness onto to a clean black scrub test panel and allowed to dry horizontally in a conditioned room at 23°C ± 2 °C and 75% relative humidity under a constant 2 mph air flow.

[0099] For dry time, utilized to determine no tire pick-up dry time, w¾s determined using the standard method of ASTM D711-20. A small dry time is desirable for many paint applications, including road marking applications.

Table 6: Testing results

[0100] Example Paints 1-4 showed good viscosity and scrub resistance, with acceptable drying time.

[0101] The compounds and methods of the appended claims are not limited in scope by the specific compounds and methods described herein, which are intended as illustrations of a few aspects of the claims and any compounds and methods that are functionally equivalent are within the scope of this disclosure. Various modifications of the compounds and methods in addition to those shown and described herein are intended to fall within the scope of the appended claims. Further, while only certain representative compounds, methods, and aspects of these compounds and methods are specifically described, other compounds and methods are intended to fall within the scope of the appended claims. Thus, a combination of steps, elements, components, or constituents can be explicitly mentioned herein; however, all other combinations of steps, elements, components, and constituents are included, even though not explicitly stated.

EMBODIMENTS

[0102] As used below, any reference to a series of embodiments is to be understood as a reference to each of those embodiments disjunctively (e.g., "Illustrative embodiments 1-4" is to be understood as "illustrative embodiments 1, 2, 3, or 4").

[0103] Illustrative embodiment 1 is a polymer according to Formula 1:

Formula 1 wherein each of m, n, and p is independently a number from 0.5 to 500; each of R₁, R₂, and R3 is independently - H or C₁-C₄ alkyl; R4 is an amine-substituted C1-C6 alkyl; 5₁ is -H or C₁- C₆ alkyl; Rg is substituted or unsubstituted C₁-C₆, alkyl; each of X16 X3, X5, and X6 is independently S, O, or N; each of X2, X4, X₇, and X8 is independently S or O; Y is CH₂, CS, or CO; and each of L₁ and L₂ is independently^ substituted or unsubstituted C₁-C₆ alkyd.

[0104] Illustrative embodiment 2 is the polymer of any preceding or subsequent illustrative embodiment, wherein R4 is selected from the group consisting CH₂CH₂NH₂ , - CH₂CH₂N(CH3)2 , and -CH₂CH₂N(CH₂CH3)₂.

[0105] Illustrative embodiment 3 is the polymer of any preceding or subsequent illustrative embodiment, wherein L₁ and L₂ are independently selected from the group consisting of -CH₂-; -CH₂CH₂-; and -CFI₂CH₂CH₂-.

[0106] Illustrative embodiment 4 is the polymer of any preceding or subsequent illustrative embodiment, wherein L1 is -CH₂CH₂-.

[0107] Illustrative embodiment 5 is the polymer of any preceding or subsequent illustrative embodiment, wherein R6 is -CH₃. [0108] Illustrative embodiment 6 is the polymer of any preceding or subsequent illustrative embodiment, wherein each of X₁-X8 is O, and wherein Y is CO.

[0109] Illustrative embodiment 7 is the polymer of any preceding or subsequent illustrative embodiment, wherein R₁, R₂, and R3 are -CH₃.

[0110] Illustrative embodiment 8 is the polymer of any preceding or subsequent illustrative embodiment, according to Formula lx:

Formula lx wherein each of R₁, R₂, and R3 is independently -H, -CH₃, or -CH₂CH₃.

[0111] Illustrative embodiment 9 is the polymer of illustrative embodiment 8, wherein m is from 80 to 100; n is from 10 to 20; and p is from 0.5 to 2.

[0112] Illustrative embodiment 10 is the polymer of any preceding or subsequent illustrative embodiment, wherein the polymer is a random copolymer.

[0113] Illustrative embodiment 11 is a polymer formed from the formed by reacting a mixture comprising the following monomers: [0114] Illustrative embodiment 12 is the polymer of any preceding or subsequent illustrative embodiment, wherein the mixture further comprises the following monomer:

[0115] Illustrative embodiment 13 is the polymer of any preceding or subsequent illustrative embodiment, wherein the reaction is conducted at a temperature of 1 °C to 90 °C. [0116] Illustrative embodiment 14 is the polymer of any preceding or subsequent illustrative embodiment, wherein the reaction is initiated by a reducing-oxidizing pair of initiators comprising an oxidizing agent and a reducing agent.

[0117] Illustrative embodiment 15 is the polymer of any preceding or subsequent illustrative embodiment, wherein the oxidizing agent is selected from the group consisting of hydrogen peroxide, tert-butyl hydroperoxide (tBHP), ammonium persulfate (APS), sodium persulfate (SPS), and potassium persulfate (PPS), and wherein the reducing agent is selected from the group consisting of Bruggolite FF6M, Bruggolite FF7, Bruggolite E28, Bruggolite E01, Bruggolite L40, Bruggolite TP 1651, ascorbic acid, sodium formaldehyde sulfoxylate (SFS), sodium bisulfite, and sodium metabisulfite (SMBS).

[0118] Illustrative embodiment 16 is a polymer according to Formula 2: wherein each of m, n, and p is independently a number from 0.5 to 500; each of R₁, R₂, and R₃ is independently -H or C1-C4 alkyl; R₄ is an amine-substituted C₁-C₆ alkyl; R₅ is -H or C₁- C₆ alkyl; each of X₁ and X3 is independently S, O, or N; each of X2, X4, and X6, is independently S or O; each of a and b is independently a number from 0 to 4; and L₁ is -H or substituted or unsubstituted C₁-C₆ alkyl.

[0119] Illustrative embodiment 17 is a coating additive, comprising the polymer of any preceding or subsequent illustrative embodiment. [0120] Illustrative embodiment 18 is a coating composition, comprising: the polymer of any preceding or subsequent illustrative embodiment; and an amine-containing compound. [0121] Illustrative embodiment 19 is the coating composition of any preceding or subsequent illustrative embodiment, wherein the amine-containing compound comprises an amine-containing polymer.

[0122] Illustrative embodiment 20 is the coating composition of any preceding or subsequent illustrative embodiment, wherein the amine-containing compound comprises a silyl amine.

[0123] Illustrative embodiment 21 is the coating composition of any preceding or subsequent illustrative embodiment, wherein the silyl amine is selected from the group consisting of N-[3-(trimethoxysilyl)propyl]ethylenediamine, Nl-(3- trimethoxysilylpropylldiefhylenetriamine, (3 -aminopiOpyl)trimethoxysiiane, ( 3- aminopropyl)triethoxysilane, 3-(ethoxydimethylsilyl)propylamine, N-[3- (trimethoxysilyl)propyl]ethylenediamine, and aminoethylaminopropyl trimethoxysiiane. [0124] Illustrative embodiment 22 is the coating composition of any preceding or subsequent illustrative embodiment, wherein the silyl amine is aminoethylaminopropyl trimethoxysiiane .

[0125] Illustrative embodiment 23 is the coating composition of any preceding or subsequent illustrative embodiment, iurther comprising a latex that is anionically stabilized. [0126] Illustrative embodi ment 24 is the coating composition of any preceding or subsequent illustrative embodiment, wherein the polymer is present in the coating composition in an amount of 0.01-2 wt. %, based on a dry weight of the composition.

[0127] Illustrative embodiment 25 is the coating composition of any preceding or subsequent illustrative embodiment, wherein the amine-containing compound is present in the coating composition in an amount of 0.01-2 wt %, based on a dry weight of the composition.

[0128] Illustrative embodiment 26 is a paint comprising: the polymer of any preceding or illustrative embodiment; and an amine-containing compound.

[0129] Whereas particular examples of this invention have been described above for purposes of illustration, it will be evident to those skilled in the art that numerous variations of the details of the present invention may be made without departing from the invention as defined in the appended claims.

Claims

WHAT IS CLAIMED IS:

1. A polymer according to Formula 1 :

Formula 1 wherein each of m, n, and p is independently a number from 0.5 to 500; each of R₁, R₂, and R₃ is independently -H or C₁-C₄ alkyl;

R₄ is an amine-substituted C₁-C₆, alkyl;

R₅ is -H or C₁-C₆, alkyl;

Re is substituted or unsubstituted C₁-C₆ alkyl; each of X₁, X₃, X₅, and X₆ is independently S, O, or N; each of X₂, X₄, X₇, and Xs is independently S or O;

Y is CH₂, CS, or CO; and each of L₁ and L₂ is independently substituted or unsubstituted C₁-C₆ alkyl.

2. The polymer of claim 1 , wherein R4 is selected from the group consisting of -CH₂CH₂NH₂, -CH₂CH₂N(CH₃)2 , and -CH₂CH₂N(CH₂CH₃)2.

3. The polymer of claim 1 or 2, wherein L₁ and L₂ are independently selected from the group consisting of -CH₂-; -CH₂CH₂-; and -CH₂CH₂CH₂-.

4. The polymer of any one of claims 1-3, wherein L₁ is -CH₂CH₂-.

5. The polymer of any one of claims 1-4, wherein R₆ is -CH3.

6. The polymer of any one of claims 1-5, wherein each of X₁-X8 is O, and wherein Y is CO.

7. The polymer of any one of claims 1-6 wherein R₁, R₂, and R₃ are -CH3.

8. The polymer of claim 1, according to Formula lx:

Formula lx wherein each of R₁, R₂, and R:, is independently -H, -CH3, or -CH₂CH3.

9. The polymer of claim 8, wherein m is from 80 to 100; n is from 10 to 20; and p is from 0.5 to 2.

10. The polymer of any one of claims 1-9, wherein the polymer is a random copolymer.

11. A polymer formed from the formed by reacting a mixture comprising the following monomers:

12. The polymer of claim 11, wherein the mixture further comprises a monomer selected from the group consisting of: , and combinations thereof.

13. The polymer of claim 11 or 12, wherein the reaction is conducted at a temperature of 1 °C to 90 °C.

14. The polymer of any one of claims 11-13, wherein the reaction is initiated by a reducing- oxidizing pair of initiators comprising an oxidizing agent and a reducing agent.

15. The polymer of any one of claims 11-14, wherein the oxidizing agent is selected from the group consisting of hydrogen peroxide, tert-butyl hydroperoxide (tBHP), ammonium persulfate (APS), sodium persulfate (SPS), and potassium persulfate (PPS), and wherein the reducing agent is selected from the group consisting of Bruggolite FF6M, Bruggolite FF7, Bruggolite E28, Bruggolite E01, Bruggolite L40, Bruggolite TP 1651, ascorbic acid, sodium formaldehyde sulfoxylate (SFS), sodium bisulfite, and sodium metabisulfite (SMBS).

16. A polymer according to Formula 2:

Formula 2 wherein each of m, n, and p is independently a number from 0.5 to 500; each of R₁, R2, and R3 is independently -H or C1-C4 alkyl;

R4 is an amine-substituted C₁-C₆ alkyl; R.5 is -H or C1-C6 alkyl; each of X₁ and X3 is independently S, O, or N; each of X2, X4, and X₆, is independently S or O; each of a and b is independently a number from 0 to 4; and L₁ is -H or substituted or unsubstituted C₁-C₆ alkyl.

17. A coating additive, comprising the polymer of any one of claims 1-16.

18. A coating composition, comprising: the polymer of any one of claims 1-16; and an amine-containing compound.

19. The coating composition of claim 18, wherein the amine-containing compound comprises an amine-containing polymer.

20. The coating composition of claim 18 or 19, wherein the amine-containing compound comprises a silyl amine.

21. The coating composition of claim 20, wherein the silyl amine is selected from the group consisting of N-[3-(trimethoxysilyl)propyl]ethylenediamine, N1 -(3- trimethoxysilylpropyi)diethylenetriamine, (3 -ammopropyl)trimethoxysilane, (3- aminopropylltriethoxysilane, 3-(ethoxydimethylsilyl)propylamine, N-[3- (trimethoxysilyl)propyl]ethylenediamine, and aminoethylaminopropyl trimethoxysilane.

22. The coating composition of claim 20 or 21, wherein the silyl amine is aminoethylaminopropyl trimethoxysilane .

23. The coating composition of any one of claims 18-22, further comprising an anionically stabilized latex.

24. The coating composition of any one of claims 18-23, wherein the polymer is present in the coating composition in an amount of 0.01-2 wt. %, based on a dry weight of the composition.

25. The coating composition of any one of claims 18-24, wherein the amine-containing compound is present in the coating composition in an amount of 0.01-2 wt. %, based on a dry weight of the composition.

26. A paint comprising: the polymer of any one of claims 1-16; and an amine-containing compound.